Patent US4515659A successfully refreshed from Google Patents.
US4515659A
Expired / Lapsed
US
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Pyrolytic conversion of plastic and rubber waste to hydrocarbons with basic salt catalysts
Assignee: United States Department of Energy
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Filing: 1982-09-30
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Granted: 1985-05-07
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Expires: 2002-09-30
Abstract
Abstract The invention relates to a process for improving the pyrolytic conversion of waste selected from rubber and plastic to low molecular weight olefinic materials by employing basis salt catalysts in the waste mixture. The salts comprise alkali or alkaline earth compounds, particularly sodium carbonate, in an amount of greater than about 1 weight percent based on the waste feed.
Inventors
- 👤 Robert C. Wingfield, Jr.
- 👤 Jacob Braslaw
- 👤 Roy L. Gealer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 19:01
CPC Classifications
C; C10; C10B; C10B53/00; C10B53/07; Y; Y02; Y02P; Y02P20/00; Y02P20/141; Y02P20/143
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
122 words
A process for pyrolytic conversion of waste selected from the group consisting of plastic and rubber to olefinic hydrocarbons, said process being characterized by comprising: introducing into a pyrolysis zone particles of said waste and at least about 1 weight percent basic salt catalyst based on the weight of said waste; heating said waste/salt mixture in said pyrolysis zone to a temperature of between about 400° C. and about 700° C. while flowing inert gas therethrough; maintaining said temperature of said pyrolysis zone and said flowing gas for a time sufficient to pyrolyze said waste to char and volatile hydrocarboncontaining products; cooling said volatile products so as to separate said products into a gas fraction and oil fractions; and recovering said fractions.
Claim 2
Dependent Claim
122 words
A process for pyrolytic conversion of waste selected from the group consisting of plastic and rubber to olefinic hydrocarbons, said process being characterized by comprising: introducing into a pyrolysis zone particles of said waste and at least about 1 weight percent basic salt catalyst based on the weight of said waste; heating said waste/salt mixture in said pyrolysis zone to a temperature of between about 400° C. and about 700° C. while flowing inert gas therethrough; maintaining said temperature of said pyrolysis zone and said flowing gas for a time sufficient to pyrolyze said waste to char and volatile hydrocarboncontaining products; cooling said volatile products so as to separate said products into a gas fraction and oil fractions; and recovering said fractions.
Claim 3
Dependent Claim
36 words
A process for pyrolytic conversion of wastes to hydrocarbons according to claim 1, wherein said basic salt catalyst is selected from the group consisting of oxides, hydroxides and carbonates of alkali metals or alkaline earth metals.
Claim 4
Dependent Claim
32 words
A process for pyrolytic conversion of wastes to hydrocarbons according to claim 2, wherein said catalyst is selected from the group consisting of potassium carbonate, magnesium carbonate, calcium carbonate and sodium carbonate.
Claim 5
Dependent Claim
26 words
A process for pyrolytic conversion of wastes to hydrocarbons according to claim 1, wherein said basic salt catalyst has a particle size below about 0.25 mm.
Claim 6
Dependent Claim
43 words
A process for pyrolytic conversion of wastes to hydrocarbons according to claim 1, wherein basic salt catalysts soluble in water are employed as aqueous solutions thereof, said solution being admixed with said waste prior to introduction of said waste into said pyrolysis zone.
Claim 7
Dependent Claim
22 words
A process for pyrolytic conversion of wastes to hydrocarbons according to claims 3, 4, or 5, wherein said catalyst is sodium carbonate.
Claim 8
Dependent Claim
37 words
A process for pyrolytic conversion of wastes to hydrocarbon according to claim 1, wherein said catalyst is included in an amount of between about 3 and about 15 weight percent based on the weight of said waste.
Claim 9
Dependent Claim
28 words
A process for pyrolytic conversion of wastes to hydrocarbons according to claim 1, wherein said temperature of said pyrolysis zone is between about 450° and about 650° C.
Claim 10
Dependent Claim
39 words
A process for pyrolytic conversion of wastes to hydrocarbons according to claim 1, wherein said inert gas consists of a mixture of nitrogen and carbon dioxide obtained by burning a fuel gas mixture with a stoichiometric amount of air.
Claim 11
Dependent Claim
32 words
A process for pyrolytic conversion of wastes to hydrocarbons according to claim 1, wherein at least a portion of said catalyst is admixed with said waste prior to pyrolysis of said waste.
Claim 12
Dependent Claim
33 words
A process for pyrolytic conversion of wastes to hydrocarbons according to claims 1 or 10, wherein at least a portion of said catalyst is admixed with said waste during pyrolysis of said waste.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-05-06 | 1988-11-05 | 1989-05-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-05-06 | 1992-11-05 | 1993-05-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-05-06 | 1996-11-05 | 1997-05-07 | $7700.00 | Window Closed / Lapsed |